JPH0760005A - Dearation of liquid product - Google Patents
Dearation of liquid productInfo
- Publication number
- JPH0760005A JPH0760005A JP5240486A JP24048693A JPH0760005A JP H0760005 A JPH0760005 A JP H0760005A JP 5240486 A JP5240486 A JP 5240486A JP 24048693 A JP24048693 A JP 24048693A JP H0760005 A JPH0760005 A JP H0760005A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- liquid
- degassing
- dissolved
- deaeration
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0005—Degasification of liquids with one or more auxiliary substances
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】この発明は、発泡性アルコール飲
料，炭酸飲料等の飲料や、医薬品、化粧品等のように品
質保持の上で脱酸素処理が必要な液状製品から、溶存気
体、特に溶存酸素を除去する脱気方法に関するものであ
る。BACKGROUND OF THE INVENTION The present invention relates to beverages such as effervescent alcoholic beverages and carbonated beverages, and liquid products such as pharmaceuticals and cosmetics which require deoxidation treatment to maintain quality. The present invention relates to a degassing method for removing oxygen.
【０００２】[0002]
【従来の技術】周知のように、液体中の溶存酸素は酸化
の要因とされており、その液体自体が製品の場合は、液
体中の成分の劣化を引き起こし、洗浄用途等に用いる場
合には、被洗浄物を酸化させる。例えば、清酒，ワイ
ン，焼酎等の酒類や、清涼飲料、果汁飲料等において
は、飲料中に溶存する酸素の影響により、風味の劣化、
変色等が生じる。2. Description of the Related Art As is well known, dissolved oxygen in a liquid is considered to be a factor of oxidation. When the liquid itself is a product, it causes deterioration of components in the liquid, and when it is used for cleaning purposes, etc. , Oxidize the object to be cleaned. For example, in alcoholic beverages such as sake, wine, shochu, soft drinks, fruit juice drinks, etc., deterioration of flavor due to the influence of oxygen dissolved in the drink,
Discoloration occurs.
【０００３】このような現象を防止するために液状製品
中から溶存酸素を含む溶存気体を除去すれば良く、この
溶存気体の除去方法としては、曝気法（ガス置換法）、
加熱脱気法、真空脱気法、化学的脱気法等がある。しか
し、上記の各脱気方法の内、加熱脱気法においては、被
処理液体を開放系で加熱し、溶存気体を放出除去するも
のであるため、運転上の不注意や機器の不具合によって
酸素が再溶存する可能性があり、また、熱によって変質
するものには適用できず、また、化学的脱気法では、脱
酸素剤等の薬品を使用するため、その製品の風味を損な
ったり、安全性の面で問題がある。そのため、上記の様
な飲料としての液状製品では、曝気法や真空脱気法が採
用されてきた。In order to prevent such a phenomenon, the dissolved gas containing dissolved oxygen may be removed from the liquid product. As the method for removing this dissolved gas, an aeration method (gas replacement method),
There are a heating degassing method, a vacuum degassing method, a chemical degassing method, and the like. However, among the above degassing methods, in the heating degassing method, the liquid to be treated is heated in an open system to release and remove the dissolved gas. May be redissolved, and cannot be applied to those that are deteriorated by heat, and in the chemical degassing method, since a chemical such as an oxygen scavenger is used, the flavor of the product may be impaired, There is a problem in terms of safety. Therefore, for liquid products such as the above beverages, the aeration method and the vacuum deaeration method have been adopted.
【０００４】上記曝気法（ガス置換法）では、酸素以外
の高純度ガス（例えば、窒素ガス、炭酸ガス）を、曝気
槽内の被処理液体に吹き込み、高純度ガスと被処理液体
を直接接触させ、液体中の酸素分圧を下げることによ
り、物理的に溶存酸素を除去する。In the aeration method (gas replacement method), a high-purity gas other than oxygen (for example, nitrogen gas, carbon dioxide gas) is blown into the liquid to be treated in the aeration tank, and the high-purity gas and the liquid to be treated are directly contacted with each other. Then, the dissolved oxygen is physically removed by lowering the oxygen partial pressure in the liquid.
【０００５】上記真空脱気法は、脱気塔を用い、被処理
液体との接触雰囲気を真空にすることによりガス分圧を
下げ、被処理液体中の溶存気体を脱気する方法である。
近年では、真空脱気法の一つとして、水を通さず気体の
みを透過させる気体透過膜（疎水性高分子膜）を用い、
この膜を介して水中の溶存酸素を減圧下の気相へ析出さ
せる膜式真空脱気法も実用化されている。The vacuum degassing method is a method of degassing a dissolved gas in the liquid to be treated by using a degassing tower and reducing the gas partial pressure by making the contact atmosphere with the liquid to be treated vacuum.
In recent years, as one of the vacuum degassing methods, a gas permeable membrane (hydrophobic polymer membrane) that allows only gas to permeate without passing water is used.
A membrane-type vacuum degassing method in which dissolved oxygen in water is precipitated in the gas phase under reduced pressure through this membrane has also been put into practical use.
【０００６】しかし、ビール、スパークリング・ワイン
等の発泡酒や炭酸飲料のように、特定の気体（この場合
は炭酸ガス）を溶存させておく必要のある液体の場合、
上記のような真空脱気法、加熱脱気法では、溶存酸素の
みならず、この種製品としての風味の重要な要素である
炭酸ガスまで除去されてしまう。そのため、後で炭酸ガ
スを再添加する必要が生じるが、この再添加するための
炭酸ガスのコストが非常に高価である。そのため、この
ような種類の液体においては、高純度ガスとして炭酸ガ
スを用いて曝気法によって脱酸素していた。However, in the case of a liquid such as beer, sparkling wine, or other low-malt beer or carbonated beverages in which a specific gas (in this case, carbon dioxide gas) needs to be dissolved,
In the vacuum deaeration method and the heat deaeration method as described above, not only dissolved oxygen but also carbon dioxide gas, which is an important element of the flavor as a product of this kind, is removed. Therefore, it becomes necessary to re-add carbon dioxide gas later, but the cost of carbon dioxide gas for this re-addition is very high. Therefore, in such a type of liquid, carbon dioxide was used as the high-purity gas to deoxidize it by the aeration method.
【０００７】[0007]
【発明が解決しようとする課題】上記のように発泡酒や
炭酸飲料のように特定の気体（炭酸ガス）を含んだ液状
製品から溶存酸素を含む溶存気体を除去しようとする場
合、炭酸ガスを用いた曝気によって行っているが、液体
中の溶存酸素濃度を低レベルまで低減させるには、極め
て高純度の炭酸ガスを用いる必要が有り、また、被処理
液体中に吹き込む炭酸ガスの泡の大きさをなるべく小さ
くして液体とガスとの接触面積を増加させたりするなど
の工夫が必要であり、また時間も多くかかる。具体的に
は、ビールを炭酸ガスを用いて、40分間曝気しても溶存
酸素量を1ppm以下にするのは難しい。また、装置構成の
制約上、曝気は陽圧下で行われるが、雰囲気圧力が高い
と溶存酸素の除去が難しいという問題もある。When attempting to remove dissolved gas containing dissolved oxygen from a liquid product containing a specific gas (carbon dioxide gas) such as sparkling liquor and carbonated drinks as described above, carbon dioxide gas is removed. Although it is carried out by the aeration used, it is necessary to use extremely high-purity carbon dioxide gas in order to reduce the dissolved oxygen concentration in the liquid to a low level, and the size of bubbles of carbon dioxide gas blown into the liquid to be treated is large. It is necessary to take measures such as reducing the size as much as possible to increase the contact area between the liquid and gas, and it also takes a lot of time. Specifically, it is difficult to reduce the amount of dissolved oxygen to 1 ppm or less even when aerating beer with carbon dioxide for 40 minutes. Further, although aeration is performed under a positive pressure due to the restriction of the apparatus configuration, there is a problem that it is difficult to remove dissolved oxygen if the atmospheric pressure is high.
【０００８】また この曝気法は、バッチ式で行われる
ため、曝気する気体が大量に必要であるのに加え、曝気
により大量の気泡が発生し、曝気槽の有効容積が小さく
なるため、大掛かりな曝気槽が必要になる。更に、この
ような曝気槽でビール等を炭酸ガスで曝気した場合、曝
気槽上部のエア抜きより、ビールの泡が出入りするた
め、外からの菌汚染の可能性があり、衛生上も良くな
い。Further, since this aeration method is performed in a batch system, a large amount of gas to be aerated is required, and a large amount of bubbles are generated due to aeration, which reduces the effective volume of the aeration tank, resulting in a large scale. An aeration tank is required. Furthermore, when beer or the like is aerated with carbon dioxide gas in such an aeration tank, bubbles of beer flow in and out from the air bleeding at the top of the aeration tank, which may cause bacterial contamination from the outside and is not good for hygiene. .
【０００９】この発明は、上述の曝気式脱気法並びに膜
式真空脱気法の問題点を解決し、両者の長所を兼ね備え
た、低コストで且つ簡単な装置構成で、液状製品から溶
存酸素を除去することを目的としている。The present invention solves the above-mentioned problems of the aeration-type deaeration method and the membrane-type vacuum deaeration method, and has the advantages of both, and is a low-cost and simple apparatus configuration, and the dissolved oxygen from a liquid product is dissolved. The purpose is to remove.
【００１０】[0010]
【課題を解決するための手段】この発明は、上述の課題
に鑑みてなされたもので、膜式脱気法とガス置換法を組
み合わせ、真空吸引手段や、大容量の曝気槽を用いるこ
となく、気体透過膜の両側における分圧の差を利用し
て、液状製品から目的の溶存気体のみを除去するもので
ある。The present invention has been made in view of the above-mentioned problems, and combines the membrane degassing method and the gas replacement method without using a vacuum suction means or a large-capacity aeration tank. By utilizing the partial pressure difference between both sides of the gas permeable membrane, only the target dissolved gas is removed from the liquid product.
【００１１】具体的には、１乃至複数種の不活性ガスか
らなる脱気用気体を溶存させた状態の液状製品を被脱気
処理液体とし、この被脱気処理液体を気体透過膜の一方
の側に流通させると共に、他方の側を脱気気体の放出空
間として、この被脱気処理液体中の脱気用気体を気体透
過膜を介して放出空間側に移動させると同時にこの脱気
用気体と共に溶存気体を放出空間側に移動させ、脱気処
理を行なうことを第１の特徴とし、更に、上記気体透過
膜を介して放出空間に移動した気体から、脱気用気体を
回収し、上記脱気処理後の液状製品に添加することを第
２の特徴とする液状製品の脱気方法である。Specifically, a liquid product in which a degassing gas consisting of one or a plurality of inert gases is dissolved is used as a degassed liquid, and the degassed liquid is used as one of the gas permeable membranes. The degassing gas in the liquid to be degassed is moved to the discharge space side through the gas permeable membrane, while the other side is used as the degassing gas discharge space. The first feature is that the dissolved gas is moved to the release space side together with the gas, and the degassing process is performed. Furthermore, the degassing gas is recovered from the gas that has moved to the release space through the gas permeable membrane, A second feature of the liquid product degassing method is to add the liquid product after the degassing treatment.
【００１２】[0012]
【作用】この発明によれば、被処理液体を、１乃至複数
種の不活性ガスからなる脱気用気体を、好ましくは過飽
和状態まで溶存させた状態とし、気体透過膜の一方の側
に流通させ、他方の側を脱気用気体及び溶存気体の放出
空間とすることにより、上記脱気用気体による気泡と被
処理液体中の他の溶存気体の分圧差により当該気泡内に
溶存気体を取り込み、上記気体透過膜を介して脱気用気
体と共に溶存気体を系外に除去する。According to the present invention, the liquid to be treated is dissolved in a degassing gas composed of one or more kinds of inert gas, preferably to a supersaturated state, and is passed to one side of the gas permeable membrane. By setting the other side as a discharge space for the degassing gas and the dissolved gas, the dissolved gas is taken into the bubbles due to the partial pressure difference between the bubbles due to the degassing gas and the other dissolved gas in the liquid to be treated. The dissolved gas is removed out of the system together with the degassing gas through the gas permeable membrane.
【００１３】[0013]
【実施例】以下、この発明方法の一実施例について説明
する。まず、不活性ガスのうちから、脱気処理を行う液
状製品（以下、被処理液体という）について、その被処
理液体中の成分を変化させない適宜の気体（不活性ガ
ス）を１乃至複数種を選択し、脱気用気体とする。ここ
で、上記の不活性ガスとは、反応性の乏しい気体、即
ち、広義の不活性ガスであって、希ガスの他、窒素、二
酸化炭素（炭酸ガス）等を含む。また、上記脱気用気体
を得るにあたって、上記選択した不活性ガスが１種類の
場合はそのまま用い、複数種のものにおいては、適宜の
組成比率でもって混合しておく。EXAMPLE An example of the method of the present invention will be described below. First, among inert gases, for a liquid product to be degassed (hereinafter referred to as a liquid to be treated), one or more kinds of appropriate gas (inert gas) that does not change the components in the liquid to be treated are selected. Select and use as degassing gas. Here, the above-mentioned inert gas is a gas with poor reactivity, that is, an inert gas in a broad sense, and includes nitrogen, carbon dioxide (carbon dioxide gas), etc. in addition to a rare gas. Further, in obtaining the degassing gas, when the selected inert gas is one kind, it is used as it is, and when plural kinds are selected, they are mixed in an appropriate composition ratio.
【００１４】そしてこの脱気用気体を、上記被処理液体
に対して吹き込み、溶存させる。この際、被処理液体に
対する溶存の程度は過飽和状態が好ましい。即ち、被処
理液体に対しての脱気用気体の量は、完全に溶存状態と
なる量以上を吹き込み、脱気用気体の一部が、気泡（微
細なほど好ましい）となった状態である。そして、気体
透過膜の一方の側を大気開放状態の放出空間とし（以
下、この側を気相側と称す。）、他方の側に上記の被処
理液体を流通させる（以下、この側を液相側と称
す。）。The degassing gas is blown into and dissolved in the liquid to be treated. At this time, the degree of dissolution in the liquid to be treated is preferably supersaturated. That is, the amount of the degassing gas with respect to the liquid to be treated is a state in which the degassing gas is blown in such an amount that it is completely dissolved, and a part of the degassing gas becomes bubbles (finer is more preferable). . Then, one side of the gas permeable membrane is used as a discharge space in an open state to the atmosphere (hereinafter, this side is referred to as a gas phase side), and the liquid to be treated is circulated to the other side (hereinafter, this side is a liquid Called the side.)
【００１５】すると、被処理液体中に過飽和状態で存在
する脱気用気体は、気体透過膜の一側を流通する過程に
おいて、気泡として析出し、気体透過膜を通過して気相
側に移動する。このときの被処理液体中の脱気用気体の
挙動に注目すると、まず、脱気用気体は被処理液体中に
微細な気泡として析出するが、この際の気泡の周囲の被
処理液体中には、この脱気用気体以外に溶存酸素等の他
の溶存気体が存在している。即ち、この微細な気泡内
は、殆どが脱気用気体であって、周囲の被処理液体中に
溶存する脱気用気体以外の分圧は殆ど０となっている。
上記の気泡が析出し、成長する過程では、この気泡と被
処理液体の界面において、両側の気体成分の分圧比が均
一になるようにガス移動が行われ、従って、被処理液体
中の脱気用気体以外の溶存気体は、脱気用気体の気泡内
に取り込まれた後、気体透過膜を介して脱気用気体と共
に放出空間中に放出されることになる。従って、本発明
方法は、ミクロ的に視点に立てば、曝気法の改良であ
り、従来バッチ式でしか行なえなかった曝気法を連続的
に行え、しかも、曝気に用いる気体量を大幅に減少でき
ることになる。Then, the degassing gas existing in a supersaturated state in the liquid to be treated is deposited as bubbles in the process of flowing through one side of the gas permeable membrane, passes through the gas permeable membrane and moves to the gas phase side. To do. Focusing on the behavior of the degassing gas in the liquid to be treated at this time, first, the degassing gas precipitates as fine bubbles in the liquid to be treated. In addition to the degassing gas, other dissolved gas such as dissolved oxygen exists. That is, most of the fine bubbles are degassing gas, and the partial pressure of the degassing gas other than the degassing gas dissolved in the liquid to be treated is almost zero.
In the process in which the bubbles are deposited and grow, the gas is moved at the interface between the bubbles and the liquid to be treated so that the partial pressure ratios of the gas components on both sides become uniform. The dissolved gas other than the working gas is taken into the bubbles of the degassing gas and then released into the discharge space together with the degassing gas through the gas permeable membrane. Therefore, the method of the present invention is an improvement of the aeration method from a microscopic viewpoint, can continuously perform the aeration method which can be performed only by the conventional batch method, and can significantly reduce the amount of gas used for the aeration. become.
【００１６】次に、この発明を適用した基本的な装置の
一構成例を図１を参照しながら説明する。図面におい
て、脱気モジュール(10)は、図面に模式的に示すよう
に、内部に中空糸状或いは平膜状等の気体透過膜(11)を
収容したもので、この気体透過膜(11)によって脱気モジ
ュール(10)の内部空間を被処理液体を流通させる液相側
(L) と、大気開放状態の放出空間とする気相側(G) とに
区画してある。この脱気モジュール(10)の液相側(L) の
一端には被処理液体の供給ライン(13)を、他端には処理
液体の排出ライン(14)を接続してあり、気相側(G) は大
気開放としてある。上記被処理液体の供給ライン(13)に
は、脱気用気体の供給する気体供給ライン(15)を接続し
てあり、この気体供給ライン(15)から上記被処理液体中
に脱気用気体を供給するようにしてある。Next, one structural example of a basic device to which the present invention is applied will be described with reference to FIG. In the drawing, the degassing module (10) contains a gas permeable membrane (11) in the form of a hollow fiber or a flat membrane, as schematically shown in the drawing. Liquid phase side through which the liquid to be treated flows through the internal space of the degassing module (10)
It is divided into (L) and the gas phase side (G) which is the release space in the open state. The liquid line side (L) of this degassing module (10) is connected to the supply line (13) of the liquid to be treated and the other end to the discharge line (14) of the liquid to be treated. (G) is open to the atmosphere. The supply line (13) for the liquid to be treated is connected to a gas supply line (15) for supplying a gas for degassing, and the gas for degassing is introduced into the liquid to be treated from the gas supply line (15). Is supplied.
【００１７】上記の構成において、気体供給ライン(15)
から脱気用気体を被処理液体の供給ライン(13)中に供給
し、脱気用気体が過飽和状態となるまで被処理液体中に
吹き込み溶存させる。この状態の被処理液体を供給ライ
ン(13)から脱気モジュール(10)内の液相側(L) に供給す
ると、この液相側(L) を通過する過程において被処理液
体中に脱気用気体が気泡として析出する。そして、この
脱気用気体の気泡の成長過程において、被処理液体中の
他の溶存気体を気泡内に取り込んだ後、この脱気用気体
は溶存酸素等の溶存気体を取り込んだ脱気用気体は気体
透過膜を介してこの溶存気体と共に放出空間（気相側
(G) ）に放出され、実質的に脱酸素される。In the above structure, the gas supply line (15)
The degassing gas is supplied from the above into the liquid to be treated supply line (13), and is blown and dissolved in the liquid to be treated until the degassing gas becomes supersaturated. When the liquid to be treated in this state is supplied from the supply line (13) to the liquid phase side (L) in the degassing module (10), the liquid to be treated is degassed in the process of passing through this liquid phase side (L). The working gas is deposited as bubbles. Then, during the growth process of the bubbles of the degassing gas, after the other dissolved gas in the liquid to be treated is taken into the bubbles, the degassing gas is the degassing gas that has taken in the dissolved gas such as dissolved oxygen. Is a discharge space (gas phase side) with this dissolved gas through the gas permeable membrane.
(G)) and is substantially deoxygenated.
【００１８】更に、以上の説明では、気体透過膜の気相
側は大気開放状態の放出空間としてあり、溶存酸素等の
溶存気体は、脱気用気体と共に大気中に放出している
が、本発明の第２の特徴は、上記気体透過膜の気相側か
ら放出される全気体のうちから上記脱気用気体を回収
し、この回収した脱気用気体を上記液状製品に再添加す
るようにしたことである。この脱気用気体の再添加は、
脱気処理前の液状製品に対して行なう場合は、脱気用気
体の消費量を更に削減することができる。Further, in the above description, the gas phase side of the gas permeable membrane is a release space open to the atmosphere, and dissolved gas such as dissolved oxygen is released into the atmosphere together with the degassing gas. A second feature of the invention is that the degassing gas is recovered from all the gases released from the gas phase side of the gas permeable membrane, and the recovered degassing gas is re-added to the liquid product. That is what I did. The re-addition of this degassing gas is
When the liquid product before the degassing process is performed, the consumption amount of the degassing gas can be further reduced.
【００１９】また、液状製品に元々含まれている気体を
脱気用気体として利用して脱気処理を行なう場合、例え
ば、ビール、炭酸飲料等の様な炭酸ガスを含んでいる液
状製品において、この炭酸ガスを脱気用気体として利用
する場合は、上記回収した脱気用気体を脱気後の液状製
品に再添加する。この場合、脱気後の液状製品は上記の
ように溶存酸素等の溶存気体が除去されているため、こ
の再添加に際して、脱気処理前よりも多量の脱気用気体
（炭酸ガス）を添加することができる。When the gas originally contained in the liquid product is used as a degassing gas for degassing, for example, in a liquid product containing carbon dioxide gas such as beer and carbonated drinks, When this carbon dioxide gas is used as a degassing gas, the recovered degassing gas is added again to the degassed liquid product. In this case, since dissolved gas such as dissolved oxygen has been removed from the liquid product after degassing as described above, when re-adding, add a larger amount of degassing gas (carbon dioxide gas) than before degassing. can do.
【００２０】また、上記気体透過膜の気相側から放出さ
れる全気体から上記脱気用気体を回収するに際しては、
この気体を脱酸素剤などを充填した回収容器に流通さ
せ、酸素のみを補集するようにしても良い。When recovering the degassing gas from the total gas discharged from the gas phase side of the gas permeable membrane,
This gas may be passed through a recovery container filled with an oxygen scavenger or the like to collect only oxygen.
【００２１】次に、この発明に係る脱気方法について、
より具体的な適用例を図２を参照しながら以下に説明す
る。図示する実施例は、炭酸ガスを含有する液状製品と
してビールを被処理液体とした場合を示すものである。
この実施例においては、ビール中に、炭酸ガスが多量に
しかも過飽和状態で含まれるため、脱気用気体としてこ
の炭酸ガスを用いることができ、従って、この場合は、
脱気用気体の添加操作を省略することができる。Next, regarding the degassing method according to the present invention,
A more specific application example will be described below with reference to FIG. The illustrated embodiment shows the case where beer is used as the liquid to be treated as a liquid product containing carbon dioxide gas.
In this example, since carbon dioxide gas was contained in beer in a large amount and in a supersaturated state, this carbon dioxide gas could be used as the degassing gas. Therefore, in this case,
The operation of adding the degassing gas can be omitted.
【００２２】周知のように、醗酵直後のビール原液は、
酵母により酸素が消費されており、溶存酸素は実質上含
まれないが、後工程の濾過工程において、空気の巻込み
等によって、この際に酸素が溶存する。そのため、この
濾過工程とこの工程以降に設けられる容器への充填工程
との間に脱気工程を設ける。As is well known, the beer stock solution immediately after fermentation is
Oxygen is consumed by yeast and dissolved oxygen is not substantially contained, but oxygen is dissolved at this time due to air entrainment in the subsequent filtration step. Therefore, a deaeration step is provided between this filtration step and the step of filling the container provided after this step.
【００２３】この脱気工程においては、被処理液体の流
通経路中に、上記と同様の脱気モジュール(10)と、この
脱気モジュール(10)と略同様の構成を有する気体再添加
用モジュール(20)を配置してある。即ち、上記の脱気モ
ジュール(10)は、上記したように内部に気体透過膜(11)
を収容し、この気体透過膜(11)によって内部空間を被処
理液体を流通させる液相側(L1)と、脱気用気体が放出さ
れる気相側(G1)とに区画したものである。また、上記気
体再添加用モジュール(20)は、内部に気体透過膜(21)を
収容し、この気体透過膜(21)によって内部空間を被処理
液体を流通させる液相側(L2)と、再添加する脱気用気体
を流通させる気相側(G2)とに区画したものである。In this degassing step, a degassing module (10) similar to the above and a gas re-adding module having substantially the same structure as the degassing module (10) are provided in the flow path of the liquid to be treated. (20) is arranged. That is, the degassing module (10) has the gas permeable membrane (11) inside as described above.
The gas permeable membrane (11) is used to store the internal space, and the internal space is divided into a liquid phase side (L1) through which the liquid to be treated flows and a gas phase side (G1) from which the degassing gas is released. . Further, the gas re-addition module (20) contains a gas permeable membrane (21) inside, and a liquid phase side (L2) for circulating the liquid to be treated through the internal space by the gas permeable membrane (21), It is divided into the gas phase side (G2) through which the degassing gas to be added again flows.
【００２４】上記脱気モジュール(10)の液相側(L1)の一
端には被処理液体の供給ライン(13)を、他端には脱気処
理液の排出ライン(14)を接続してあり、気相側(G1)は脱
気用気体の回収装置(30)に接続してある。A supply line (13) for the liquid to be treated is connected to one end of the liquid phase side (L1) of the degassing module (10), and a discharge line (14) for the degassed treatment liquid is connected to the other end. The gas phase side (G1) is connected to the degassing gas recovery device (30).
【００２５】上記気体再添加用モジュール(20)の液相側
(L2)の一端は上記脱気モジュール(10)からの脱気処理液
の排出ライン(14)を、他端には気体添加処理液の排出ラ
イン(22)を接続してあり、気相側(G2)には上記脱気用気
体回収装置(30)からの脱気用気体の再添加供給ライン(3
1)を接続してある。Liquid phase side of the gas re-addition module (20)
One end of (L2) is connected to the discharge line (14) of the degassing treatment liquid from the degassing module (10), and the other end is connected to the discharge line (22) of the gas addition treatment liquid, the gas phase side (G2) is a re-addition supply line (3) for the degassing gas from the degassing gas recovery device (30).
1) is connected.
【００２６】上記脱気用気体回収装置(30)は、この実施
例においては少なくとも酸素を捕捉すれば良いため、例
えば、脱酸素剤、吸着剤等を収納した構成とすることが
できる。In the present embodiment, the degassing gas recovery device (30) has only to capture at least oxygen, so that it can be constructed to contain, for example, a deoxidant, an adsorbent and the like.
【００２７】上記再添加供給ライン(31)の上流には、更
に、添加用気体の供給装置(40)が上記回収装置(30)と並
列に接続してある。ここで、この添加用気体は、対象と
する液状製品がビールであり、炭酸ガスである。An addition gas supply device (40) is further connected in parallel with the recovery device (30) upstream of the re-addition supply line (31). Here, the target liquid product of this additive gas is beer and is carbon dioxide gas.
【００２８】上記構成において、濾過工程終了後のビー
ルを、被処理液体供給ライン(13)から脱気モジュール(1
0)に供給すると、この脱気モジュール(10)内の液相側(L
1)の被処理液体から気相側(G1)に向けて、脱気用気体と
しての炭酸ガスが溶存酸素と共に析出して脱気用気体回
収装置(30)に流入し、この脱気処理後のビールは、排出
ライン(14)から気体再添加用モジュール(20)に流入す
る。In the above-mentioned structure, the beer after the filtration step is degassed from the liquid to be treated supply line (13) by the degassing module (1).
0), the liquid phase side (L
From the liquid to be treated in 1) toward the gas phase side (G1), carbon dioxide gas as a degassing gas is precipitated together with dissolved oxygen and flows into the degassing gas recovery device (30), and after this degassing treatment. Of the beer flows into the gas re-addition module (20) through the discharge line (14).
【００２９】気体再添加用モジュール(20)においては、
液相側(L2)に脱気処理後のビールが流入し、気相側(G2)
には、脱気用気体回収装置(30)により少なくとも酸素を
除去した脱気気体（ほとんど炭酸ガスである）が流入す
る。このとき、気体再添加用モジュール(20)の液相側(L
2)には、再添加供給ライン(31)を介して添加用気体の供
給装置(40)からの炭酸ガスが供給されている。In the gas re-addition module (20),
Beer after degassing has flowed into the liquid phase side (L2), and the gas phase side (G2)
A degassed gas (mostly carbon dioxide) from which at least oxygen has been removed by the degassing gas recovery device (30) flows into the chamber. At this time, the liquid phase side (L
Carbon dioxide gas is supplied to 2) from the supply gas supply device (40) for addition via the re-addition supply line (31).
【００３０】気体再添加用モジュール(20)の液相側(L2)
を流れるビールには、上記とは逆に、気相側(G2)の炭酸
ガスが溶け込む。Liquid phase side of the gas re-addition module (20) (L2)
Contrary to the above, carbon dioxide gas on the gas phase side (G2) dissolves in the beer flowing in the direction.
【００３１】従って、この脱気後のビールは、以後の工
程、並びに、工場出荷後の流通過程において、溶存酸素
による風味の劣化が防止できる。Therefore, the degassed beer can be prevented from deteriorating the flavor due to dissolved oxygen in the subsequent steps and in the distribution process after shipment from the factory.
【００３２】この脱気処理の際に消費される炭酸ガスの
量は、従来の炭酸ガス曝気による脱気酸素方法に比べ、
極めて少量で済む。The amount of carbon dioxide gas consumed in this degassing treatment is larger than that in the conventional degassing oxygen method by aeration of carbon dioxide gas.
Very small amount.
【００３３】更に、従来の曝気による脱気方法では、大
掛かりな曝気槽設備が必要であり、また、バッチ式でし
か脱気処理を行えないが、この発明によれば、以上のよ
うな簡単な小型の設備で、連続的な脱気処理を行うこと
ができる。Further, in the conventional degassing method by aeration, a large-scale aeration tank facility is required, and deaeration processing can be performed only in a batch system. It is possible to perform continuous degassing with a small facility.
【００３４】実際に、従来の曝気法とに本発明による方
法とで、ビールを同程度にまで脱気処理した場合の炭酸
ガスの消費量を比較すると、ビール 1キロリットル当たり、曝
気法では 350リットルの消費であるが、本発明によると36〜
44リットルと、その消費量が約 1/8〜1/10程度に激減した。Actually, when comparing the conventional aeration method and the method according to the present invention with respect to the amount of carbon dioxide gas consumed when degassing beer to the same degree, it was found that 350 kg / kg of beer was consumed by the aeration method. The consumption of the liter is 36-according to the present invention.
The consumption was 44 liters, which was drastically reduced to about 1/8 to 1/10.
【００３５】更に、液状製品から除去された脱気用気体
は回収装置にて溶存酸素を分離した後再添加するように
してあるため、この操作により炭酸ガスの使用量は、更
に、従来の数％程度まで低減可能である。Further, since the degassing gas removed from the liquid product is added again after the dissolved oxygen is separated by the recovery device, the amount of carbon dioxide gas used by this operation is further reduced from the conventional one. % Can be reduced.
【００３６】尚、以上の適用例以外にも、その他の発泡
性のワイン，焼酎等の酒類、その他の飲料、醤油等の液
体調味料、化粧液等の液状製品や、それらの原料液とし
ての濃縮原液、割り水等の製造ライン中においても容易
に適用することができる。In addition to the above-mentioned application examples, other sparkling wines, liquors such as shochu, other beverages, liquid seasonings such as soy sauce, liquid products such as cosmetic liquids, and raw materials thereof are used. It can be easily applied even in the production line for concentrated stock solutions, split water, etc.
【００３６】[0036]
【発明の効果】この発明によれば、１乃至複数種の不活
性ガスからなる脱気用気体を溶存させた状態の液状製品
を被脱気処理液体とし、この被脱気処理液体を気体透過
膜の一方の側に流通させると共に、他方の側を脱気気体
の放出空間として、この被脱気処理液体中の脱気用気体
を気体透過膜を介して放出空間側に移動させると同時に
この脱気用気体と共に溶存気体を放出空間側に移動さ
せ、脱気処理を行なうことができるため、従来、曝気法
によるしかなかった液状製品の脱気処理を、簡単な構成
の小型の装置で容易に、しかも連続して行える。又、従
来の曝気法によると大量の高純度ガス（或は所定組成の
ガス）を消費していたが、この発明によればその消費量
を大幅に削減することができる。According to the present invention, a liquid product in which a degassing gas composed of one or a plurality of inert gases is dissolved is used as a degassed liquid, and the degassed liquid is gas permeable. While flowing to one side of the membrane, the other side is used as a release space for the degassed gas, and the degassing gas in the liquid to be degassed is moved to the release space side through the gas permeable membrane and at the same time. Since the dissolved gas can be moved to the release space side together with the degassing gas to perform the degassing process, the degassing process of liquid products, which was conventionally only possible by the aeration method, can be easily performed with a small device with a simple structure. And it can be done continuously. Further, according to the conventional aeration method, a large amount of high-purity gas (or gas having a predetermined composition) is consumed, but according to the present invention, the consumption amount can be significantly reduced.
【００３７】更に、このガスを回収して再利用するよう
にしたため、より一層その消費量を削減でき、液状製品
自体が所定の気体を含有するものであってもこの再添加
によって実質上溶存酸素のみを除去することが可能とな
る。Furthermore, since this gas is collected and reused, the consumption amount can be further reduced, and even if the liquid product itself contains a predetermined gas, this re-addition substantially eliminates dissolved oxygen. Only this can be removed.
【００３８】更に、気体透過膜の使用により、曝気法に
比べ、液相側と気相側の接触面積を増大させることがで
きるため、脱気効率が高い。Further, by using the gas permeable membrane, the contact area between the liquid phase side and the gas phase side can be increased as compared with the aeration method, so that the degassing efficiency is high.
【図１】この発明に係る一実施例を示す概略構成図であ
る。FIG. 1 is a schematic configuration diagram showing an embodiment according to the present invention.
【図２】この発明に係る他の実施例を示す概略構成図で
ある。FIG. 2 is a schematic configuration diagram showing another embodiment according to the present invention.
(10) 脱気モジュール (11) 気体透過膜 (13) 被処理液体供給ライン (14) 排出ライン (15) 気体供給ライン (20) 気体再添加用モジュール (21) 気体透過膜 (22) 排出ライン (30) 脱気用気体回収装置 (31) 再添加供給ライン (10) Degassing module (11) Gas permeable membrane (13) Liquid to be treated supply line (14) Discharge line (15) Gas supply line (20) Gas re-addition module (21) Gas permeable membrane (22) Discharge line (30) Degassing gas recovery device (31) Re-addition supply line
Claims (2)
あって、１乃至複数種の不活性ガスからなる脱気用気体
を溶存させた状態の液状製品を被脱気処理液体とし、こ
の被脱気処理液体を気体透過膜の一方の側に流通させる
と共に、他方の側を脱気気体の放出空間として、この被
処理液体中の脱気用気体を気体透過膜を介して放出空間
側に移動させると同時にこの脱気用気体と共に溶存気体
を放出空間側に移動させ、脱気処理を行なうことを特徴
とする液状製品の脱気方法。1. A method for removing dissolved gas from a liquid product, wherein a liquid product in which a degassing gas composed of one or more kinds of inert gas is dissolved is used as a degassed liquid, The degassed liquid is circulated to one side of the gas permeable film, and the other side is used as a degassing gas discharge space, and the degassing gas in the liquid to be processed is discharged to the discharge space side through the gas permeable film. A method for degassing a liquid product, which comprises moving the dissolved gas together with the degassing gas to the discharge space side for degassing.
あって、１乃至複数種の不活性ガスからなる脱気用気体
を溶存させた状態の液状製品を被脱気処理液体とし、こ
の被脱気処理液体を気体透過膜の一方の側に流通させ、
他方の側を脱気用気体及び溶存気体の放出空間とし、上
記気体透過膜を介して放出空間に移動した気体から、脱
気用気体を回収し、上記脱気処理後の液状製品に添加す
ることを特徴とする液状製品の脱気方法。2. A method for removing a dissolved gas from a liquid product, wherein a liquid product in which a degassing gas composed of one or a plurality of inert gases is dissolved is used as a degassed liquid, The degassed liquid is circulated to one side of the gas permeable membrane,
The other side is used as a discharge space for the degassing gas and the dissolved gas, and the degassing gas is recovered from the gas that has moved to the discharge space through the gas permeable membrane and added to the liquid product after the degassing treatment. A degassing method for liquid products, which is characterized in that
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5240486A JPH0760005A (en) | 1993-08-31 | 1993-08-31 | Dearation of liquid product |
| CA002131148A CA2131148A1 (en) | 1993-08-31 | 1994-08-30 | Method for deaerating liquid products |
| US08/298,619 US5522917A (en) | 1993-08-31 | 1994-08-31 | Method for deaerating liquid products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5240486A JPH0760005A (en) | 1993-08-31 | 1993-08-31 | Dearation of liquid product |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0760005A true JPH0760005A (en) | 1995-03-07 |
Family
ID=17060235
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5240486A Pending JPH0760005A (en) | 1993-08-31 | 1993-08-31 | Dearation of liquid product |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US5522917A (en) |
| JP (1) | JPH0760005A (en) |
| CA (1) | CA2131148A1 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08318138A (en) * | 1995-05-26 | 1996-12-03 | Mitsubishi Heavy Ind Ltd | Degasifier |
| JP2000107511A (en) * | 1998-10-02 | 2000-04-18 | Kurita Water Ind Ltd | Decarbonation treating method |
| JP2006231328A (en) * | 2005-02-23 | 2006-09-07 | United Technol Corp <Utc> | Membrane based de-oxygenator for process stream |
| JP2007243113A (en) * | 2006-03-13 | 2007-09-20 | Kurita Water Ind Ltd | Production method, production device, and washing device for gas dissolution washing water |
| JP2008521596A (en) * | 2004-11-30 | 2008-06-26 | ファイア テクノロジーズ、インコーポレイテッド | Contacting device and method and use thereof |
| JP2018047426A (en) * | 2016-09-21 | 2018-03-29 | オルガノ株式会社 | Deoxidation treatment method and deoxidation treatment system of water to be treated and production method of deoxidized carbonated water containing hardness component |
| JP2020517282A (en) * | 2017-04-24 | 2020-06-18 | クアーズ ブリューイング カンパニー | System and method for producing beer/hard cider concentrate |
Families Citing this family (34)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5762684A (en) * | 1995-11-30 | 1998-06-09 | Dainippon Screen Mfg. Co., Ltd. | Treating liquid supplying method and apparatus |
| US5922249A (en) * | 1995-12-08 | 1999-07-13 | Novartis Ag | Ophthalmic lens production process |
| JPH11137907A (en) * | 1997-11-11 | 1999-05-25 | Moore Kk | Deaerator |
| US6248157B1 (en) * | 1999-08-20 | 2001-06-19 | Systec Inc. | Vacuum degassing |
| US6228146B1 (en) | 2000-03-03 | 2001-05-08 | Don R. Kuespert | Gas recovery device |
| US6391096B1 (en) | 2000-06-09 | 2002-05-21 | Serveron Corporation | Apparatus and method for extracting and analyzing gas |
| US6558450B2 (en) * | 2001-03-22 | 2003-05-06 | Celgard Inc. | Method for debubbling an ink |
| US6726743B2 (en) | 2002-06-18 | 2004-04-27 | 3M Innovative Properties Company | Electrostatic deaeration method and apparatus |
| US6939392B2 (en) * | 2003-04-04 | 2005-09-06 | United Technologies Corporation | System and method for thermal management |
| TW200505554A (en) * | 2003-04-22 | 2005-02-16 | Mykrolis Corp | Pleated construction for effecting gas transfer membrane |
| AU2004249161B9 (en) | 2003-06-13 | 2010-04-08 | Covidien Lp | Multiple member interconnect for surgical instrument and absorbable screw fastener |
| US6949132B2 (en) * | 2003-11-05 | 2005-09-27 | Systel, Llc | Axial degassing transfer lines |
| US7713331B2 (en) * | 2003-11-05 | 2010-05-11 | Rheodyne, Llc | Axial transfer line degassing |
| JP4526335B2 (en) * | 2004-09-07 | 2010-08-18 | セイコーエプソン株式会社 | Droplet discharge device |
| US7459081B2 (en) * | 2004-11-30 | 2008-12-02 | Phyre Technologies, Inc. | Contacting systems and methods and uses thereof |
| US7393388B2 (en) * | 2005-05-13 | 2008-07-01 | United Technologies Corporation | Spiral wound fuel stabilization unit for fuel de-oxygenation |
| US7435283B2 (en) * | 2005-05-18 | 2008-10-14 | United Technologies Corporation | Modular fuel stabilization system |
| US7465336B2 (en) * | 2005-06-09 | 2008-12-16 | United Technologies Corporation | Fuel deoxygenation system with non-planar plate members |
| US7377112B2 (en) | 2005-06-22 | 2008-05-27 | United Technologies Corporation | Fuel deoxygenation for improved combustion performance |
| US20070101731A1 (en) * | 2005-09-07 | 2007-05-10 | United Technologies Corporation | Deoxygenated fuel-cooled environmental control system pre-cooler for an aircraft |
| US7615104B2 (en) * | 2005-11-03 | 2009-11-10 | United Technologies Corporation | Fuel deoxygenation system with multi-layer oxygen permeable membrane |
| US20070130956A1 (en) * | 2005-12-08 | 2007-06-14 | Chen Alexander G | Rich catalytic clean burn for liquid fuel with fuel stabilization unit |
| US7569099B2 (en) * | 2006-01-18 | 2009-08-04 | United Technologies Corporation | Fuel deoxygenation system with non-metallic fuel plate assembly |
| US7824470B2 (en) * | 2006-01-18 | 2010-11-02 | United Technologies Corporation | Method for enhancing mass transport in fuel deoxygenation systems |
| US7582137B2 (en) * | 2006-01-18 | 2009-09-01 | United Technologies Corporation | Fuel deoxygenator with non-planar fuel channel and oxygen permeable membrane |
| US7882704B2 (en) * | 2007-01-18 | 2011-02-08 | United Technologies Corporation | Flame stability enhancement |
| US20090020013A1 (en) | 2007-07-20 | 2009-01-22 | Sloan Michael A | Membrane based deoxygenator for processing fluids |
| US8075675B2 (en) * | 2008-06-12 | 2011-12-13 | Serveron Corporation | Apparatus and method for extracting gas from liquid |
| US20100184198A1 (en) * | 2009-01-16 | 2010-07-22 | Joseph Russell T | Systems and Methods of Urea Processing to Reduce Sorbent Load |
| EP2755735A4 (en) | 2011-09-12 | 2018-01-24 | Idex Health & Science LLC | Supersaturated fluid degassing |
| US9687773B2 (en) | 2014-04-30 | 2017-06-27 | Honeywell International Inc. | Fuel deoxygenation and fuel tank inerting system and method |
| US9656187B2 (en) | 2014-11-12 | 2017-05-23 | Honeywell International Inc. | Fuel deoxygenation system contactor-separator |
| US9834315B2 (en) | 2014-12-15 | 2017-12-05 | Honeywell International Inc. | Aircraft fuel deoxygenation system |
| US9897054B2 (en) | 2015-01-15 | 2018-02-20 | Honeywell International Inc. | Centrifugal fuel pump with variable pressure control |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3574987A (en) * | 1970-02-18 | 1971-04-13 | Mojonnier Bros Co | Vacuum deaerator device |
| JPS5423081A (en) * | 1977-07-25 | 1979-02-21 | Boeicho Gijutsu Kenkyu Honbuch | Method of manufacturing nearly pure oxygen from water together with discharging generated carbon dioxide into water |
| JPS551816A (en) * | 1978-06-15 | 1980-01-09 | Mitsubishi Rayon Co Ltd | Vapor-liquid contactor |
| DE3304951A1 (en) * | 1983-02-12 | 1984-08-16 | Akzo Gmbh, 5600 Wuppertal | DEVICE FOR FILTERING A LIQUID |
| US5143526A (en) * | 1985-10-11 | 1992-09-01 | Sepracor, Inc. | Process of treating alcoholic beverages by vapor-arbitrated pervaporation |
| JPS62204086A (en) * | 1986-03-04 | 1987-09-08 | 株式会社エルマ、シーアール | Pipe |
| JPS63302926A (en) * | 1987-05-30 | 1988-12-09 | Eruma:Kk | Device for replacing dissolved gas in liquid |
| JPH03118802A (en) * | 1989-10-02 | 1991-05-21 | Dainippon Ink & Chem Inc | Deoxidizing device |
| JP2877923B2 (en) * | 1990-09-07 | 1999-04-05 | オルガノ株式会社 | Removal method of dissolved gas in liquid |
| JP2898080B2 (en) * | 1990-11-02 | 1999-05-31 | 日東電工株式会社 | Operation method of degassing membrane device |
| JPH089034B2 (en) * | 1991-02-22 | 1996-01-31 | 株式会社荏原総合研究所 | Method for removing dissolved oxygen from pure water or ultrapure water |
-
1993
- 1993-08-31 JP JP5240486A patent/JPH0760005A/en active Pending
-
1994
- 1994-08-30 CA CA002131148A patent/CA2131148A1/en not_active Abandoned
- 1994-08-31 US US08/298,619 patent/US5522917A/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08318138A (en) * | 1995-05-26 | 1996-12-03 | Mitsubishi Heavy Ind Ltd | Degasifier |
| JP2000107511A (en) * | 1998-10-02 | 2000-04-18 | Kurita Water Ind Ltd | Decarbonation treating method |
| JP2008521596A (en) * | 2004-11-30 | 2008-06-26 | ファイア テクノロジーズ、インコーポレイテッド | Contacting device and method and use thereof |
| JP2006231328A (en) * | 2005-02-23 | 2006-09-07 | United Technol Corp <Utc> | Membrane based de-oxygenator for process stream |
| JP2007243113A (en) * | 2006-03-13 | 2007-09-20 | Kurita Water Ind Ltd | Production method, production device, and washing device for gas dissolution washing water |
| WO2007105820A1 (en) * | 2006-03-13 | 2007-09-20 | Kurita Water Industries Ltd. | Process and equipment for production of wash water containing dissolved gas, and cleaning equipment |
| US8123833B2 (en) | 2006-03-13 | 2012-02-28 | Kurita Water Industries Ltd. | Process for producing gas-containing cleaning water, apparatus for producing the cleaning water and cleaning apparatus |
| JP2018047426A (en) * | 2016-09-21 | 2018-03-29 | オルガノ株式会社 | Deoxidation treatment method and deoxidation treatment system of water to be treated and production method of deoxidized carbonated water containing hardness component |
| JP2020517282A (en) * | 2017-04-24 | 2020-06-18 | クアーズ ブリューイング カンパニー | System and method for producing beer/hard cider concentrate |
| US11802261B2 (en) | 2017-04-24 | 2023-10-31 | Porifera, Inc. | System and method for producing beer/hard cider concentrate |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2131148A1 (en) | 1995-03-01 |
| US5522917A (en) | 1996-06-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH0760005A (en) | Dearation of liquid product | |
| SU1194284A3 (en) | Method of preparing completely fermented low-alcohol beverages | |
| CA3061006C (en) | System and method for producing beer/hard cider concentrate | |
| JPS59125885A (en) | Concentration fo alcohol benerage | |
| JPH0780205A (en) | Selective deaeration and its device | |
| WO1992008783A1 (en) | Membrane process for the dealcoholization of naturally fermented beverages | |
| US4664918A (en) | Process for reducing alcohol in fermented beverages by means of dialysis | |
| DK167157B1 (en) | Process for partially or totally dealcoholizing wine and/or cider, and appliance for implementing the process | |
| US6981997B2 (en) | Deaeration of water and other liquids | |
| US4015020A (en) | Tartar removal by electrodialysis and potassium level control in wine | |
| JPH0824561B2 (en) | Method for producing low alcohol beer | |
| US5817359A (en) | Methods for dealcoholization employing perstration | |
| CN115667486A (en) | Single-serving capsule for preparing alcoholic beer | |
| US3988486A (en) | Method for accelerating the crystallization and removal of tartar from a tartarous beverage | |
| EP1164185A2 (en) | Method and apparatus for reducing foaming during fermentation | |
| JP2018047426A (en) | Deoxidation treatment method and deoxidation treatment system of water to be treated and production method of deoxidized carbonated water containing hardness component | |
| JPH07185211A (en) | Method and apparatus for member type aeration | |
| US7455777B2 (en) | Method of adjusting levels of dissolved compounds in beverages | |
| JP2000014378A (en) | Production of rice wines | |
| EP0057785B1 (en) | Process for the preparation of a flavored alcoholic beverage | |
| JPH07222553A (en) | Method for degassing tea drink | |
| SU1082803A1 (en) | Method for making wines saturated with carbon dioxide | |
| WO2002028994A1 (en) | Method of removing carbon dioxide from fermenting medium using a polymeric membrane | |
| Sengupta et al. | Membrane Contactor Applications in Various Industries | |
| JPH07265055A (en) | Fine filteration of beer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |